EP2746397A1 - Fabrication d'acides gras oméga-aminés - Google Patents

Fabrication d'acides gras oméga-aminés Download PDF

Info

Publication number
EP2746397A1
EP2746397A1 EP12199024.6A EP12199024A EP2746397A1 EP 2746397 A1 EP2746397 A1 EP 2746397A1 EP 12199024 A EP12199024 A EP 12199024A EP 2746397 A1 EP2746397 A1 EP 2746397A1
Authority
EP
European Patent Office
Prior art keywords
fatty acid
whole
cell catalyst
recombinant
oxo
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP12199024.6A
Other languages
German (de)
English (en)
Inventor
Steffen Schaffer
Jasmin GIELEN
Mirja Wessel
Hans-Georg Hennemann
Harald HÄGER
Thomas Haas
Wilfried BLÜMKE
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Evonik Industries AG
Original Assignee
Evonik Industries AG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Evonik Industries AG filed Critical Evonik Industries AG
Priority to EP12199024.6A priority Critical patent/EP2746397A1/fr
Priority to HUE13194396A priority patent/HUE034426T2/en
Priority to ES13194396.1T priority patent/ES2640712T3/es
Priority to EP13194396.1A priority patent/EP2746399B1/fr
Priority to SG10201605082RA priority patent/SG10201605082RA/en
Priority to SG2013092010A priority patent/SG2013092010A/en
Priority to MX2013014727A priority patent/MX349714B/es
Priority to KR1020130157998A priority patent/KR102252150B1/ko
Priority to US14/132,473 priority patent/US9719117B2/en
Priority to CN201310707410.5A priority patent/CN103881933B/zh
Priority to ARP130104951A priority patent/AR094464A1/es
Priority to BR102013033208A priority patent/BR102013033208A2/pt
Priority to JP2013265665A priority patent/JP6332961B2/ja
Publication of EP2746397A1 publication Critical patent/EP2746397A1/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P13/00Preparation of nitrogen-containing organic compounds
    • C12P13/001Amines; Imines
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N15/00Mutation or genetic engineering; DNA or RNA concerning genetic engineering, vectors, e.g. plasmids, or their isolation, preparation or purification; Use of hosts therefor
    • C12N15/09Recombinant DNA-technology
    • C12N15/11DNA or RNA fragments; Modified forms thereof; Non-coding nucleic acids having a biological activity
    • C12N15/52Genes encoding for enzymes or proenzymes
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P13/00Preparation of nitrogen-containing organic compounds
    • C12P13/005Amino acids other than alpha- or beta amino acids, e.g. gamma amino acids
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/14Fungi; Culture media therefor
    • C12N1/16Yeasts; Culture media therefor
    • C12N1/18Baker's yeast; Brewer's yeast
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/20Bacteria; Culture media therefor
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/0004Oxidoreductases (1.)
    • C12N9/0008Oxidoreductases (1.) acting on the aldehyde or oxo group of donors (1.2)
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/0004Oxidoreductases (1.)
    • C12N9/0012Oxidoreductases (1.) acting on nitrogen containing compounds as donors (1.4, 1.5, 1.6, 1.7)
    • C12N9/0014Oxidoreductases (1.) acting on nitrogen containing compounds as donors (1.4, 1.5, 1.6, 1.7) acting on the CH-NH2 group of donors (1.4)
    • C12N9/0016Oxidoreductases (1.) acting on nitrogen containing compounds as donors (1.4, 1.5, 1.6, 1.7) acting on the CH-NH2 group of donors (1.4) with NAD or NADP as acceptor (1.4.1)
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/0004Oxidoreductases (1.)
    • C12N9/0069Oxidoreductases (1.) acting on single donors with incorporation of molecular oxygen, i.e. oxygenases (1.13)
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/10Transferases (2.)
    • C12N9/1096Transferases (2.) transferring nitrogenous groups (2.6)
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/10Transferases (2.)
    • C12N9/12Transferases (2.) transferring phosphorus containing groups, e.g. kinases (2.7)
    • C12N9/1288Transferases for other substituted phosphate groups (2.7.8)
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/64Fats; Fatty oils; Ester-type waxes; Higher fatty acids, i.e. having at least seven carbon atoms in an unbroken chain bound to a carboxyl group; Oxidised oils or fats
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/582Recycling of unreacted starting or intermediate materials

Definitions

  • the invention relates to a whole-cell catalyst which expresses a recombinant ⁇ -dioxygenase or the combination of a recombinant fatty acid reductase and a fatty acid reductase phosphopantheteinylierenden phosphopantheteinyl transferase, and which additionally expresses a transaminase, wherein the phosphopanthaemyl transferase and / or transaminase is preferably recombinant; and a process for reacting a fatty acid, ⁇ -hydroxy fatty acid, ⁇ -oxo fatty acid or a monoester thereof to an amine, comprising the steps of oxidizing the fatty acid, ⁇ -hydroxy fatty acid, ⁇ -oxo fatty acid or monoester thereof Contacting with an alkane hydroxylase and / or alcohol dehydrogenase to an oxidation product contacting the oxidation product with a phosphopantheylated
  • Polyamides are a class of polymers characterized by repeating amide groups.
  • Polyamides are derived from primary amines or secondary amines conventionally obtained from cracking hydrocarbons. However, it is also possible to use derivatives, more particularly aminocarboxylic acids, lactams and diamines, for polymer production. Also of interest are short-chain, gaseous alkanes as starting materials, which can be obtained from renewable raw materials using biotechnological processes.
  • polyamide 6 can be obtained by polymerizing ⁇ -caprolactam and "polyamide 12" by polymerizing laurolactam.
  • Other commercially interesting products include copolymers of lactam, e.g. B. Copolymers of ⁇ -caprolactam and laurolactam.
  • Suitable sources of renewable resources are, in particular, sources of fatty acids which can be obtained in the form of rapeseed oil, thistle oil, palm kernel oil, coconut oil, sunflower seed oil and similar natural products from a large number of biological sources, in particular from plants.
  • PCT / EP 2008/067447 describes a biotechnological system for producing chemically related products, more specifically ⁇ -aminocarboxylic acids, using a cell which has a number of suitable enzymatic activities and is capable of converting carboxylic acids to corresponding ⁇ -aminocarboxylic acid.
  • the process comprises a cascade of enzymatically catalyzed reactions, in particular the oxidation of a fatty acid on the terminal carbon atom to the aldehyde and the subsequent amination using a transaminase and an amino acid as amine donor, which can be regenerated via an amino acid dehydrogenase.
  • a known disadvantage of the alkBGT oxidase system of Pseudomonas putida GPO1 used in this case is that it is unable to afford a selective oxidation of aliphatic alkanes to primary alcohols. Rather, a variety of oxidation products occur; In particular, the proportion of more highly oxidized products such as the corresponding aldehyde, ketone or the corresponding carboxylic acid increases with increasing reaction time ( C. Grant, JM Woodley and F. Baganz (2011), Enzymes and Microbial Technology 48, 480-486 ), which correspondingly reduces the yield of the desired amine.
  • a further disadvantage of this process is that over-oxidized by-products, for example the dicarboxylic acid of the fatty acid used as starting material, the recycling of hydrophobic solvents and hydrophobic liquid cation exchangers, which according to the PCT / EP2011 / 071491 can be used to separate the product from the aqueous reaction mixture at the expense of resource efficiency.
  • the skilled person can limit and decisive factors in a system such as in the PCT / EP2008 / 067447 not routinely identified. If the yield of product is too low, this may be due to the fact that one of the enzymes is present in too low a concentration, without it being known which of the enzymes in question is involved, ie the starting material is within the intended timeframe or unreacted by degradation by competing enzymes due to insufficient synthetic capacity. Alternatively, it is quite possible that an enzyme is detectably present in the cell in the form of a polypeptide, but especially in this cell does not have the essential for the activity of folding or missing a hitherto unknown, but for the activity essential cofactor. Likewise, as already mentioned, the metabolic product can be toxic to the cell or degraded. Finally, interfering interactions with endogenous enzymes, ie naturally present in a cell used as a whole-cell catalyst, are to be expected.
  • the object underlying the invention is to provide a biotechnological process for producing ⁇ -amino fatty acids which is as efficient as possible with regard to yield, carbon balance and / or nitrogen balance and / or purity.
  • Another object of the invention is to provide as efficient as possible a biotechnological process for the conversion of carboxylic acid esters to aminated carboxylic acid esters with respect to yield, carbon and / or nitrogen balance, reusability used and / or purity of the product.
  • an efficient carbon and / or nitrogen balance is preferably understood to mean that the highest possible proportion of the carbon and / or nitrogen fed to a cell for reacting a carboxylic ester in the form of suitable substrates is found in the desired end product, instead of, for example, others Products to be implemented as the desired.
  • Another object of the invention is to improve the workability of a multiphase reaction mixture from the reaction of a carboxylic acid ester, especially with regard to the reusability for working up used hydrophobic solvent and liquid cation exchanger, as well as with regard to the phases education and separation at a biphasic system comprising an aqueous phase in which the reaction of the carboxylic acid ester takes place, and an organic phase with organic solvents and / or liquid cation exchangers.
  • the problem underlying the invention is solved in a first aspect by a whole-cell catalyst expressing a recombinant ⁇ -dioxygenase or the combination of a recombinant fatty acid reductase and a fatty acid reductase phosphopantheteinylierenden Phosphopantheteinyl transferase, and additionally expressing a transaminase, said Phosphopantheteinyl transferase and / or transaminase is preferably recombinant.
  • the problem is solved by a whole-cell catalyst which additionally expresses an amino acid dehydrogenase, which is preferably recombinant.
  • the problem is solved by a whole-cell catalyst which additionally expresses an alkane hydroxylase, which is preferably recombinant.
  • a whole-cell catalyst which additionally expresses a polypeptide of the AlkL family, which is preferably recombinant.
  • a whole-cell catalyst which additionally expresses an alcohol dehydrogenase, which is preferably recombinant.
  • a whole-cell catalyst wherein the activity of at least one enzyme participating in the ⁇ -oxidation is reduced compared to the wild type of the whole-cell catalyst.
  • the problem is solved by a whole-cell catalyst wherein the activity of BioH or a variant thereof is reduced over the wild type of the whole-cell catalyst.
  • a seventh embodiment which is also an embodiment of the first to sixth embodiments, the problem is solved by a whole-cell catalyst wherein the activity of FadL or a variant thereof is increased over the wild-type all-cell catalyst.
  • the problem underlying the invention is solved by a method wherein at step c) an amino acid dehydrogenase is present.
  • the problem is solved by a method wherein at least one enzyme from the group comprising phosphopantheteinylated fatty acid reductase, ⁇ -dioxygenase, transaminase, amino acid dehydrogenase and alkane hydroxylase, preferably all enzymes used from this group, in the form of a whole-cell catalyst according to the first aspect of the invention.
  • at least one enzyme from the group comprising phosphopantheteinylated fatty acid reductase, ⁇ -dioxygenase, transaminase, amino acid dehydrogenase and alkane hydroxylase, preferably all enzymes used from this group, in the form of a whole-cell catalyst according to the first aspect of the invention.
  • the problem is solved by a method wherein the fatty acid, ⁇ -hydroxy fatty acid, ⁇ -oxo fatty acid or the monoester thereof is a compound of the formula ( I) R 1 - A - COOR 2 (I) where R 1 is selected from the group comprising -H, -CHO, -OH and COOR 3 , wherein R 2 and R 3 are each and independently selected from the group comprising H, methyl, ethyl and propyl, with the proviso that at least one of R 2 and R 3 is H, wherein A represents a straight, branched, linear, cyclic, substituted or unsubstituted hydrocarbon group having at least four carbon atoms.
  • A has the formula - (CH 2 ) n -, where n is at least 4, preferably at least 10.
  • the problem underlying the invention is solved by using the whole-cell catalyst according to the first aspect or the method according to the second aspect for aminating a fatty acid, ⁇ -hydroxy fatty acid, ⁇ -oxo-fatty acid or a monoester thereof.
  • the problem underlying the invention is solved by a reaction mixture comprising the whole-cell catalyst according to the first aspect in aqueous solution and a fatty acid, ⁇ -hydroxy fatty acid, ⁇ -oxo-fatty acid or a monoester thereof of the formula (I) R 1 - A - COOR 2 (I), wherein R 1 is selected from the group comprising -H, -CHO, -OH and COOR 3 , wherein R 2 and R 3 are each and independently selected from the group comprising H, methyl, ethyl and propyl, with the proviso that at least one of R 2 and R 3 is H, wherein A represents an unbranched, branched, linear, cyclic, substituted or unsubstituted hydrocarbon group having at least four carbon atoms, preferably the formula - (CH 2 ) n -, wherein n is at least 4, more preferably at least 10.
  • the present invention is based on the discovery of the inventors that a functionally coexpressed recombinant fatty acid reductase or ⁇ -dioxygenase surprisingly increases the yield of ⁇ -amino-fatty acids in a whole-cell catalyst used for the production of ⁇ -amino fatty acids from fatty acids and has corresponding enzyme endowment.
  • the present invention is based on the discovery of the inventors that a functionally coexpressed recombinant fatty acid reductase or ⁇ -dioxygenase in a whole-cell catalyst, which is used for the production of ⁇ -amino fatty acids from fatty acids and having a corresponding enzyme equipment, surprisingly the concentration of interfering by-products, in particular of over-oxidized fatty acids in the form of dicarboxylic acids and esters thereof, reduced in the resulting product.
  • the present invention is based on the discovery of the inventors that a functionally co-expressed recombinant fatty acid reductase or ⁇ -dioxygenase in a whole-cell catalyst used to produce ⁇ -amino fatty acids from fatty acids and having appropriate enzyme endowment, the purity and reusability of liquid cation exchangers such Improved oleic acid used to remove an ⁇ -amino fatty acid from a fermentation solution comprising the whole-cell catalyst.
  • the present invention relates to an improved process for reacting a fatty acid, ⁇ -hydroxy fatty acid, ⁇ -oxo fatty acid or a monoester thereof to an amine, which is characterized in that, in addition to the enzymes, the transfer of the fatty acid over its various oxidation states catalyze to the amine, at least one Fatty acid reductase or ⁇ -dioxygenase, or the combination of both enzymes, is present when a whole cell catalyst is used to perform the method.
  • fatty acid reductase refers to an enzyme which refers to the conversion of an ⁇ -carboxy acid, also called dicarboxylic acid or ⁇ -carboxy fatty acid, to the corresponding ⁇ -oxo fatty acid with consumption of ATP and NAD (P) H catalyzes.
  • ⁇ -carboxy acid also called dicarboxylic acid or ⁇ -carboxy fatty acid
  • P NAD
  • fatty acid reductases are described for the preparation of ⁇ -hydroxy fatty acids, but not as part of a system for producing ⁇ -amino fatty acids.
  • the fatty acid reductase is selected from the group of fatty acid reductases having the amino acid sequences YP_887275.1, ZP_11001941.1, ZP_06852401.1, NP_959974.1, YP_001070587.1, ZP_05217435.1, YP_882653.1, YP_639435.1, ZP_10800193.1, YP_006452763.1, YP_006730440.1, ZP_11196216.1, YP_005349252.1, ZP_05224908.1, YP_005338837.1, YP_006307000.1, YP_005343991.1, ZP_11001942.1, ZP_09979565.1, YP_005003162.1, YP_953393.
  • ZP_14237669.1 ZP_09165547.1, YP_004019203.1, ZP_14240225.1, YP_001220863.1, CBA74242.1, ZP_12994240.1, EIE27140.1, ZP_15354547.1, ZP_15432557.1, ZP_15500132.1, ZP_15478632.1, ZP_06846978.
  • 1, ZP_12994610.1, ZP_07664023.1, ZP_15446620.1, ZP_15484174.1, ZP_14240245.1, YP_005358845.1 and XP_002669159.1, in particular YP_006731697.1, ZP_09839660.1, YP_001704097.1, YP_889972.1, ZP_05045132.1 , ZP_09794557.1, ZP_08240521.1, NP_959974.1, ZP_10456477.1, YP_118225.1, NP_217106, YP_905678.1, YP_887275.1, ZP_11001941.1, YP_953393.1 and YP_005349252.1 include variants thereof.
  • Fatty acid reductases are a group of enzymes that require phosphopantheylation for their activity, that is, the covalent attachment of a phosphopantheteinyl cofactor to the enzyme. Accordingly, the fatty acid reductase used in the present invention is phosphopantheylated, and a whole cell catalyst expressing the fatty acid reductase is expressed, either as part of its endogenously expressed enzyme or recombinant form, a phosphopantheyl-transferase phosphatantheylating the fatty acid reductase.
  • phosphopantheyl-transferase refers to an enzyme that has a phosphopantheethyl radical of a Phosphopantheteinyl-CoA on an enzyme, preferably on the fatty acid reductase, transmits.
  • the phosphopantheyl-transferase is selected from the group of phosphopantheyl-transferases which have the amino acid sequences AB183656.1, YP_006811024.1, YP_120266.1, YP_005265173.1, YP_004006671.1, ZP_08152482.1, ZP_11104141.1, ZP_14482198.1, YP_706581.1, ZP_10002626.1, ZP_09308410.1, YP_002783881.1, ZP_18276502.1, ZP_09271851.1, ZP_08204640.1, YP_002766085.1, ZP_09788717.1, ZP_09799863.1, ZP_10961877.1, YP_003273299.
  • the whole-cell catalyst may also have an ⁇ -dioxygenase.
  • ⁇ -dioxygenase as used herein means an enzyme that converts a fatty acid consuming one molecule of oxygen and splits off a carbon dioxide molecule to one at the terminal ⁇ -carbon atom opposite to the starting material fatty acids are truncated by one carbon atom, catalyses an aldehyde group - bearing fatty acid at the terminal ⁇ - carbon atom.
  • the ⁇ -dioxygenase is selected from the group of ⁇ -dioxygenases which have the amino acid sequences NP_001066718.1, EAY82977.1, BAH79993.1, ABG22011.1, BAJ90503.1, AFD04418.1, AFD04417.1, BAJ87736.1, AFW75180.1, ABG22012.1, XP_002311389.1, CAH05011.1, XP_002279884.1, CBI34957.3, AAG59584.1, NP_001234414.1, NP_001234410.1, XP_003553942.1, XP_002275161.1, XP_003553937.1, CB134960.3, CAA07589.1, XP_003543402.
  • the whole-cell catalyst according to the invention necessarily has a transaminase which amines the ⁇ -oxo fatty acid.
  • transaminase as used herein means an enzyme which catalyzes the transfer of ⁇ -amino groups from a donor, preferably an amino acid, to an acceptor molecule, preferably an ⁇ -ketocarboxylic acid.
  • the transaminase is from the A group of transaminases selected which have the amino acid sequences 3HMU_A, AAD41041.1, AAK15486.1, ABE03917.1, ADR60699.1, ADR61066.1, ADR62525.1, AEL07495.1, CAZ86955.1, EFW82310.1, EFW87681.1, EGC99983.1, EGD03176.1, EGE58369.1, EGH06681.1, EGH08331.1, EGH24301.1, EGH32343.1, EGH46412.1, EGH55033.1, EGH62152.1, EGH67339.1, EGH70821.1, EGH71404.
  • the fatty acid reductase used according to the invention and preferably also other enzymes used according to the invention are recombinant enzymes.
  • the term "recombinant" as used herein means that the nucleic acid molecule coding for the corresponding enzyme does not occur in the natural cell and / or it was produced using genetic engineering methods.
  • a recombinant cell as used herein is understood to mean a cell having at least one recombinant nucleic acid or a recombinant polypeptide.
  • the whole cell catalyst which can be used according to the invention is not subject to any restrictions, provided that it can be cultivated, stable and, where appropriate, genetically modified, eg. B.
  • a method for mitigating enzyme activities, such as knock outs, is accessible. So it can equally be a prokaryotic or eukaryotic cell.
  • unicellular eukaryotes are particularly preferred, especially yeasts such as Saccharomyces cerevisiae, Candida tropicalis, Candida albicans and Pichia pastoris.
  • prokaryotic cells it may be, for example, a bacterium selected from the group consisting of Magnetococcus, Mariprofundus, Acetobacter, Acetobacterium, Acidiphilium, Afipia, Ahrensia, Asticcacaulis, Aurantimonas, Azorhizobium, Azospirillum, Bacillus, Bartonella, tribocorum, Beijerinckia, Bradyrhizobium, Brevundimonas, subvibrioides, Brucella, Caulobacter, Chelativorans, Citreicella, Citromicrobium, Clostridium, Corynebacterium, Dinoroseobacter, Erythrobacter, Fulvimarina, Gluconacetobacter, Granulibacter, Hirschia, Hoeflea, Hyphomicrobium, Hyphomonas, Ketogulonicigenium, Labrenzia, Loktanella, Magnetospirillum, Maricaulis, Marit
  • subtilis B. megaterium, C. glutamicum, E. coli, Pseudomonas sp., Pseudomonas fluorescens, Pseudomonas putida, Pseudomonas stutzeri , Acinetobacter sp., Burkholderia sp., Burkholderia thailandensis, cyanobacteria, Klebsiella sp., Klebsiella oxytoca, Salmonella sp., Rhizobium sp. and Rhizobium meliloti . In a particularly preferred embodiment, it is an enterobacterium, most preferably Escherichia coli.
  • the whole-cell catalyst according to the invention in addition to fatty acid reductase, phosphopantheyl-transferase and transaminase, also has an alanine dehydrogenase in order to regenerate the alanine from inorganic nitrogen-containing molecules consumed by the transaminase during the amination of the ⁇ -oxo fatty acid.
  • alanine dehydrogenase as used herein is understood to mean an enzyme which catalyzes the conversion of L-alanine to water, NAD + to pyruvate, ammonia and NADH and the reverse reaction.
  • alanine dehydrogenase is selected from the group of alanine dehydrogenases which have the amino acid sequence of alanine dehydrogenase from Bacillus subtilis (database code L20916), Rhizobium leguminosarum (database code CP001622), Vibrio proteolyticus (database code AF070716), Mycobacterium tuberculosis (database code X63069), Enterobacter aerogenes (database code AB013821), EGR93259.1, YP_003654745.1, YP_003651439.1, YP_003637111.1, YP_003631815.1, YP_001327051.1, YP_001262560.1, YP_886996.1, YP_882850.1, YP_704410.1, YP_703508.1, ZP_08624689.1, YP_001230376.1, P17
  • alanine dehydrogenase For the reaction catalyzed by alanine dehydrogenase, the presence of not only pyruvate formed as part of the primary metabolism of each cell in question as a whole-cell catalyst is required, but also of ammonium.
  • the latter is typically provided in the form of inorganic nitrogen salts, for example, ammonium salts, nitrates, or the like.
  • an ammonium salt is added to the aqueous reaction medium, for example ammonium chloride.
  • the whole-cell catalyst according to the invention expresses an alkane hydroxylase and optionally further enzymes essential for the activity of the alkane hydroxylase, in particular for the case that a fatty acid having an oxidation state at the terminal .omega.-carbon atom is used as substrates for producing the .omega.-amino fatty acid , which is below the oxidation state of the aldehyde.
  • the alkane hydroxylase and / or an additionally expressed alcohol dehydrogenase then oxidize the terminal carbon atom to the aldehyde group, which can then be aminated by the transaminase.
  • the term "alkane hydroxylase” as used herein means an enzyme which catalyzes the hydroxylation of unsubstituted linear alkyl radicals comprising at least six, preferably twelve, carbon radical groups.
  • the alkane hydroxylase is a cytochrome P450 monooxygenase of the CYP153 family.
  • the term "cytochrome P450 monooxygenase of the CYP153 family” means a cytosolic oxidase which is part of a 3-component system which further comprises a ferredoxin and a ferredoxin reductase, with an alkane binding site and the Ability to use alkanes hydroxylate.
  • it is an enzyme which has at least 80, preferably 90, most preferably 95 or 99 percent sequence identity to the cytochrome P450 monooxygenase of the CYP153 family from Alcanivorax borkumensis SK2 (database code YP_691921) or to an enzyme, which comprises a polypeptide sequence having at least 80, preferably 90, most preferably 95 or 99 percent sequence identity to the cytochrome P450 monooxygenase of the CYP153 family from Alcanivorax borkumensis SK2 (database code YP_691921) and also has alkane hydroxylase activity.
  • cytochrome P450 monooxygenase of the CYP153 family means a non-membrane-bound oxidase which has a binding site for alkanes, unsubstituted linear alkyl radicals comprising at least five, preferably twelve carbon radical or monohydric alkanes and their polypeptide chain the motif LL (I / L) (V / I) GGNDTTRN.
  • a "cytochrome P450 monooxygenase of the CYP153 family” as used herein is a CYP153 family cytochrome P450 monooxygenase from Alcanivorax borkumensis SK2 (database code YP_691921) or a variant thereof, preferably alkanhydroxylase activity having.
  • the cell express the monooxygenase together with functionally interacting ferredoxin reductase and functionally interacting ferredoxin. This may be isolated or when using a whole-cell catalyst to co-expressed polypeptides or at the N- or C-terminal with the cytochrome P450 monooxygenase of the CYP153 family fused polypeptides.
  • ferredoxin reductase or a ferredoxin functionally interacts with a given cytochrome P450 monooxygenase of the CYP153 family
  • one skilled in the art can readily determine whether the reducing agent is more efficient in the presence of an alkane substrate and the three polypeptides than if at least one of the three is missing, oxidized.
  • the method described by Scheps, D., Malca, H., Hoffmann, B., Nestl, B.M, and Hauer, B. (2011) Org. Biomol. Chem., 9, 6727 can be used, which shows a significant increase in the rate of reaction in the case of functionally interacting polypeptides.
  • the CYP153 family cytochrome P450 monooxygenase, ferredoxin and ferredoxin reductase are from the same organism.
  • it is the ferredoxin reductase from Alcanivorax borkumensis SK2 (database code YP_691923) or a variant thereof, the ferredoxin from Alcanivorax borkumensis SK2 (database code YP_691920) or a variant thereof and the cytochrome P450 monooxygenase of the CYP153 family from Alcanivorax borkumensis SK2 (database code YP_691921) or a variant thereof.
  • the alkane hydroxylase is an alkB monooxygenase.
  • AlkB represents an oxidoreductase first known from the AlkBGT system from Pseudomonas putida Gpo1, which is dependent on two further polypeptides, AlkG and AlkT.
  • AlkT is characterized as FAD-dependent rubredoxin reductase, which transfers electrons from NADH to AlkG.
  • AlkG is a rubredoxin, an iron-containing redox protein that acts as a direct electron donor for AlkB.
  • AIkB monooxygenase means a polypeptide having a sequence homology of at least, in order of increasing preference, 75, 80, 85, 90, 92, 94, 96, 98 or 99% to the sequence of the AlkB of Pseudomonas putida Gpo1 (database code: CAB54050.1; this database code, like all other prior art used in the application, namely from the NCBI database, more specifically the release available online on 15 October 2012) having the ability to bind alkanes oxidize.
  • the alkB monooxygenase is a alkane oxidizing oxidoreductase which interacts functionally with the alkG (CAB54052.1) and alkT (CAB54063.1) polypeptides from Pseudomonas putida Gpo1.
  • the cell monooxygenase is expressed together with functionally interacting with Hilfsproteinen, preferably AlkG and / or AlkT or each variants thereof, which in turn is AlkG in a particularly preferred embodiment (CAB54052.1) and AlkT (CAB54063.1) polypeptides from Pseudomonas putida Gpo1.
  • the problem may arise that a substrate must be contacted with an intracellularly localized enzyme in order for the desired reaction to occur.
  • the whole-cell catalyst comprises a polypeptide of the AlkL family.
  • AlkL is a membrane protein from Pseudomonas putida that can import long-chain fatty acids and derivatives thereof into bacterial cells.
  • an "AlkL family polypeptide” as used herein is a polypeptide having at least 80, preferably 90, more preferably 90% sequence identity to AlkL over a length of 230 consecutive amino acids Pseudomonas putida (database code CAB69081) or a variant of Pseudomonas putida AlkL, and preferably has the ability to assist in the import of long-chain alkanes into the interior of a cell.
  • an "AlkL family polypeptide” as used herein is a polypeptide located in the outer membrane of a Gram negative bacterium having the sequence motif DXWAPAXQ (V / A) GXR, where X is a proteinogenic amino acid, and preferably additionally PALY is Pseudomonas putida (database code CAB69081) or a variant thereof.
  • Exemplary members of the AlkL family include Pseudomonas putida AlkL (database code CAB69081), Marinobacter aquaeolei VT8 (database code YP_957722), Oceanicaulis alexandrii HTCC2633 (database code ZP_00953584), Marinobacter manganoxydans Mn17-9 (database code ZP_09158756), Caulobacter sp. K31 (database code YP_001672217), Pseudomonas oleovorans (database code Q00595) and variants thereof.
  • the teaching of the present invention can be accomplished not only by using macromolecules having the exact amino acid or nucleic acid sequence referred to herein, or not only by using a cell having reduced activity of a polypeptide having the exact amino acid sequence relative to the respective wild type. but also using a variant of such macromolecules or a cell having a reduced activity relative to the respective wild-type of the respective cell of a variant of the polypeptide obtained by deletion, addition or substitution of one or more Amino acids or nucleic acids can be obtained.
  • the term "variant" of a nucleic acid sequence or amino acid sequence hereinafter synonymous and interchangeable with the term “homologue” as used herein, means another nucleic acid or amino acid sequence that comprises or represents a sequence that is useful with respect to the corresponding original wild-type nucleic acid or amino acid sequence uses a homology, here tantamount to identity, of 70, 75, 80, 85, 90, 92, 94, 96, 98, 99% or more percent, preferably other than the catalytically active center forming amino acids or structure or folding essential amino acids are deleted or substituted or merely conservative substituted, for example, a glutamate instead of an aspartate or a leucine instead of a valine.
  • the variant of an amino acid or nucleic acid sequence preferably in addition to the sequence homology mentioned above, has essentially the same enzymatic activity of the wild-type molecule or the original molecule.
  • a variant of a polypeptide enzymatically active as protease has the same or substantially the same proteolytic activity as the polypeptide enzyme, ie the ability to catalyze the hydrolysis of a peptide bond.
  • the term "substantially the same enzymatic activity” means activity with respect to the substrates of the wild-type polypeptide that is well above the background activity and / or is less than 3, more preferably 2, more preferably on the order of distinguishes the K M and / or k cat values exhibited by the wild-type polypeptide with respect to the same substrates.
  • the term "variant" of a nucleic acid or amino acid sequence comprises at least one active part or fragment of the nucleic acid or amino acid sequence.
  • the term "active part" as used herein means an amino acid sequence or nucleic acid sequence which is less than full length of the amino acid sequence or less than full length of the amino acid sequence encoding the amino acid sequence or amino acid sequence the encoded amino acid sequence of shorter length than the wild-type amino acid sequence has substantially the same enzymatic activity as the wild-type polypeptide or a variant thereof, for example as a protease.
  • the term "variant" of a nucleic acid comprises a nucleic acid whose complementary strand, preferably under stringent conditions, binds to the wild-type nucleic acid.
  • the stringency of the hybridization reaction is readily determinable by those skilled in the art and generally depends on the length of the probe, the temperatures of washing and the salt concentration. In general, longer probes require higher temperatures for hybridization, whereas shorter probes manage at low temperatures. Whether hybridization takes place depends generally from the ability of the denatured DNA to anneal to complementary strands present in their environment, below the melting temperature.
  • the stringency of hybridization reaction and corresponding conditions are more detailed in FM Ausubel (1995), Current Protocols in Molecular Biology. John Wiley & Sons, Inc. described.
  • Hybridization takes place in a preferred embodiment under stringent conditions, that is, only hybrids are formed in which the probe and target sequence, ie the polynucleotides treated with the probe, are at least 70% identical. It is known that the stringency of the hybridization including the washing steps is influenced or determined by varying the buffer composition, the temperature and the salt concentration.
  • the hybridization reaction is generally carried out at a relatively low stringency compared to the washing steps ( Hybaid Hybridization Guide, Hybaid Limited, Teddington, UK, 1996 ).
  • a buffer corresponding to 5x SSC buffer at a temperature of about 50 ° C - 68 ° C can be used.
  • probes can also hybridize with polynucleotides having less than 70% identity to the sequence of the probe. Such hybrids are less stable and are removed by washing under stringent conditions.
  • 66 ° C - 68 ° C ° C is set. Temperature ranges of about 64 ° C - 68 ° C or about 66 ° C - 68 ° C are preferred. It may be possible to lower the salt concentration to a concentration corresponding to 0.2 ⁇ SSC or 0.1 ⁇ SSC.
  • polynucleotide fragments By gradually increasing the hybridization temperature in steps of about 1 - 2 ° C from 50 ° C to 68 ° C polynucleotide fragments can be isolated, for example, in order of increasing preference at least 70% or at least 80% or at least 90%, at least 91% , at least 92%, at least 93%, at least 94%, at least 95%, at least 96%, at least 97%, at least 98% or at least 99% identity to the sequence of the nucleic acid molecule used.
  • Further instructions for hybridization are in form so-called kits available on the market (eg DIG Easy Hyb from Roche Diagnostics GmbH, Mannheim, Germany, Catalog No. 1603558 ).
  • the term "variant" of a nucleic acid as used herein includes any nucleic acid sequence encoding the same amino acid sequence as the original nucleic acid or a variant of that amino acid sequence in the context of degeneracy of the genetic code.
  • the cell used according to the invention has a reduced activity of at least one enzyme which catalyzes one of the ⁇ -oxidation reactions of fatty acids, preferably one of the group consisting of fatty acid CoA ligase , Acyl-CoA dehydrogenase, 2,4-dienoyl-CoA reductase, enoyl-CoA hydratase and 3-ketoacyl-CoA thiolase, a fatty acid importer or variants thereof.
  • Beta-oxidation of fatty acids is a widely used pathway that allows prokaryotic and eukaryotic organisms alike to oxidize fatty acids and make the chemical energy available to metabolism.
  • the fatty acid begins with the inclusion of a fatty acid in the cell.
  • the fatty acid if conditions require it, is first oxidized at the ⁇ -position of the CoA fatty acid ester by an acyl-CoA dehydrogenase, in the case of E. coli FadE.
  • an acyl-CoA dehydrogenase in the case of E. coli FadE.
  • a similar molecule can also be formed from a double unsaturated fatty acid by reduction by means of a 2,4-dienoyl-CoA reductase, in E. coli FadH.
  • coli FadB subsequently catalyzes the hydration to form the secondary alcohol and its subsequent oxidation to the ketone.
  • a 3-ketoacyl-CoA-thiolase in the case of E. coli FadA, catalyses the cleavage of the ketoacyl-CoA, with the result that acetyl-CoA and a CoA ester of the fatty acid truncated by two carbon atoms compared to the parent molecule be released. Unless it is also acetyl-CoA, the latter can be re-fed to the ⁇ -oxidation cycle and shortened under oxidation.
  • the regulation of ⁇ -oxidation of fatty acids also involves FadR, a regulator of the Fad operon that includes the genes required to degrade fatty acids without FadR catalyzing a ⁇ -oxidation reaction.
  • FadR a regulator of the Fad operon that includes the genes required to degrade fatty acids without FadR catalyzing a ⁇ -oxidation reaction.
  • the term "enzyme which catalyzes one of the ⁇ -oxidation reactions of fatty acids” means any enzyme which interacts directly with the fatty acid substrate or a molecule resulting therefrom to give the acetyl-CoA interacts, preferably recognizes as a substrate, and catalyzes its conversion to a metabolite closer to the acetyl-CoA on this degradation pathway, preferably including the fatty acid importer which effects the uptake of the fatty acid into the cell.
  • these enzymes include acyl-CoA dehydrogenase because it interacts with the fatty acid CoA ester and catalyzes its conversion to enyol-CoA, which is closer to the acetyl-CoA in the ⁇ -oxidation pathway the fatty acid CoA ester.
  • the term "enzyme that catalyses one of the ⁇ -oxidation reactions of fatty acids” as used herein means any enzyme from the group comprising the gene products FadA, FadB, FadD, FadL and FadE of E coli and / or their variants or homologs from other organisms.
  • FadA, FadB, FadD, FadL and FadE from E. coli as well as variants and homologs from numerous other biotechnologically useful organisms and their nucleic acid and polypeptide sequences are described in the prior art, for example FadA under accession number AP009048.1, FadB under accession number BAE77457.1, FadD under accession number BAA15609.1, and FadE under accession number BAA77891.2.
  • the prior art discloses numerous assays that are particularly suitable for measuring the activity of enzymes that catalyze one of the ⁇ -oxidation reactions of fatty acids, for example, in U.S. Patent Nos.
  • the substrate to be reacted preferably the fatty acid, ⁇ -hydroxy or ⁇ -oxo fatty acid
  • the substrate to be reacted preferably the fatty acid, ⁇ -hydroxy or ⁇ -oxo fatty acid
  • the enzymes required according to the invention which are located inside the whole-cell catalyst , It is therefore crucial that the substrate can get inside the cell.
  • the whole-cell catalyst expresses a fatty acid importer, in the case of a bacterial, in particular Gram-negative, whole-cell catalyst, particularly preferably the fatty acid importer FadL (database code: BAA16205.1) or a variant, preferably in one concentration and one activity , which is increased compared to the activity of the wild-type of the corresponding whole-cell catalyst.
  • a fatty acid importer in the case of a bacterial, in particular Gram-negative, whole-cell catalyst, particularly preferably the fatty acid importer FadL (database code: BAA16205.1) or a variant, preferably in one concentration and one activity , which is increased compared to the activity of the wild-type of the corresponding whole-cell catalyst.
  • Increasing the activity of a polypeptide over the wild type of the cell can be achieved by various routes routinely known to those skilled in the art. For example, the incorporation of additional, functionally linked to a promoter copies of the nucleotide sequence coding for the polypeptide or
  • the ⁇ -aminofatty acids are produced according to the invention in higher yield and purity, when the background of enzymes expressed endogenously in the whole-cell catalyst is optimized such that the activity of endogenous enzymes is reduced or eliminated, the educts, intermediates or products of the process according to the invention or using the cell according to the invention, preferably ⁇ -amino fatty acids, decompose or otherwise modify metabolic pathways that lead away from the formation of the desired product.
  • the whole-cell catalyst according to the invention has a cell which, compared to its wild type, has a reduced activity of the esterase BioH [database code YP_492020.1] or a variant thereof.
  • Such cells with reduced bioH activity, their preparation and assay for activity determination are described in the European patent application EP 12007663.3 described.
  • the whole-cell catalyst according to the invention can be used in a process for the reaction of a fatty acid, ⁇ -hydroxy or ⁇ -oxo fatty acid to the corresponding amine, preferably an ⁇ -amino fatty acid, wherein the fatty acid, ⁇ -hydroxy fatty acid, ⁇ Oxo-fatty acid or the monoester thereof to a compound of the formula (I) R 1 - A - COOR 2 (I) wherein R 1 is selected from the group consisting of -H, -CHO, -OH and COOR 3 wherein R 2 and R 3 are each and independently selected from the group comprising H, methyl, ethyl and propyl with the proviso that at least one of R 2 and R 3 is H, wherein A represents an unbranched, branched, linear, cyclic, substituted or unsubstituted hydrocarbon group having at least four carbon atoms.
  • A is a structure of the formula - (CH 2 ) n -, where n is 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 25, 26, 27, 28, 29 or 30.
  • the fatty acid, ⁇ -hydroxy or ⁇ -oxo fatty acid is lauric acid, ⁇ -hydroxy or ⁇ -oxo-lauric acid.
  • the Fatty acid, ⁇ -hydroxy or ⁇ -oxo fatty acid to hexanoic acid, ⁇ -hydroxy or ⁇ -oxo-hexanoic acid.
  • the fatty acid, ⁇ -hydroxy or ⁇ -oxo fatty acid is decanoic acid, ⁇ -hydroxy or ⁇ -oxo-decanoic acid.
  • the particular formula given includes all salts, protonated or deprotonated of the particular compound.
  • the lauric acid includes not only the protonated form but also the salt laureate with all cations, for example, sodium laureate.
  • the process according to the invention requires that the enzymes used for the process according to the invention, optionally provided in the form of the whole-cell catalyst according to the invention, are contacted with fatty acid, .omega.-hydroxy or .omega.-oxo fatty acid in an aqueous solution.
  • the term "contacting" as used herein means that the particular enzyme comes into direct contact with its substrate, in particular without intervening physical barriers such as impermeable membranes or the like. In the simplest case, the contacting takes place in that the substrate is added to an aqueous solution in which the enzyme or the whole-cell catalyst is located.
  • a reaction mixture comprising the whole-cell catalyst according to the invention in aqueous solution and a fatty acid, ⁇ -hydroxy fatty acid, ⁇ -oxo-fatty acid or a monoester thereof of the formula (I), wherein R 1 is selected from the group, which comprises -H, -CHO, -OH and COOR 3 , wherein R 2 and R 3 are each and independently selected from the group comprising H, methyl, ethyl and propyl, provided that at least one of R 2 and R 3 is H, wherein A represents an unbranched, branched, linear, cyclic, substituted or unsubstituted hydrocarbon group having at least four carbon, preferably the formula - (CH 2 ) n -, wherein n is at least 4, more preferably at least 10.
  • aqueous solution for example with regard to composition, pH and temperature, must be such that it at least temporarily supports the viability or at least the catalytic capability of the whole-cell catalyst.
  • Numerous aqueous culture media suitable as aqueous solution are known to the person skilled in the art. which are suitable for the maintenance or cultivation of cells, in particular biotechnologically significant cells. These include both full media such as LB media, minimal media such as M9 media and selective media, for example those which contain a high salt concentration and therefore only allow the growth of halophilic or at least halotolerant organisms.
  • aqueous culture medium means a water-based reaction medium which, in view of all relevant factors, in particular pH, salinity and temperature, is such that it contains the viability therein Cells, preferably microorganisms receives or promotes and both aqueous culture medium and hydrophobic organic phase in liquid form.
  • the temperature requirements of various biotechnologically significant cells can be taken from microbiological and molecular biology textbooks, eg Fuchs / Schlegl, 2008.
  • the pH of the aqueous culture medium at the time of contacting is between 4 and 9, more preferably between 4.5 and 8, 5, most preferably between 6.5 and 7.5.
  • the temperature is between 0 and 45 ° C, more preferably between 15 and 40 ° C, most preferably between 20 and 37 ° C.
  • the reaction mixture is typically contained in a fermentor.
  • the fermentor may be any reaction vessel which may be sterilized, preferably autoclaved and allowed to grow the whole-cell catalyst, aeration and control of reaction conditions such as oxygen content and temperature.
  • the reaction mixture comprises a hydrophobic organic phase in addition to the aqueous solution.
  • This may comprise an organic solvent and / or a hydrophobic liquid cation exchanger for removing the ⁇ -amino fatty acid from the aqueous solution.
  • Suitable solvents and cation exchangers are in the EP11191520.3 described.

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Zoology (AREA)
  • Wood Science & Technology (AREA)
  • Genetics & Genomics (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Biotechnology (AREA)
  • General Engineering & Computer Science (AREA)
  • Microbiology (AREA)
  • General Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Biomedical Technology (AREA)
  • Medicinal Chemistry (AREA)
  • Molecular Biology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mycology (AREA)
  • Proteomics, Peptides & Aminoacids (AREA)
  • Tropical Medicine & Parasitology (AREA)
  • Virology (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Botany (AREA)
  • Physics & Mathematics (AREA)
  • Biophysics (AREA)
  • Plant Pathology (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Enzymes And Modification Thereof (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
EP12199024.6A 2012-12-21 2012-12-21 Fabrication d'acides gras oméga-aminés Withdrawn EP2746397A1 (fr)

Priority Applications (13)

Application Number Priority Date Filing Date Title
EP12199024.6A EP2746397A1 (fr) 2012-12-21 2012-12-21 Fabrication d'acides gras oméga-aminés
HUE13194396A HUE034426T2 (en) 2012-12-21 2013-11-26 Production of Omega Amino Fatty Acids
ES13194396.1T ES2640712T3 (es) 2012-12-21 2013-11-26 Producción de ácidos omega-aminograsos
EP13194396.1A EP2746399B1 (fr) 2012-12-21 2013-11-26 Fabrication d'acides gras oméga-aminés
SG10201605082RA SG10201605082RA (en) 2012-12-21 2013-12-11 Production Of Omega-Amino Fatty Acids
SG2013092010A SG2013092010A (en) 2012-12-21 2013-12-11 Production of omega-amino fatty acids
MX2013014727A MX349714B (es) 2012-12-21 2013-12-13 Produccion de acidos grasos ?-amino.
KR1020130157998A KR102252150B1 (ko) 2012-12-21 2013-12-18 ω―아미노 지방산의 제조
US14/132,473 US9719117B2 (en) 2012-12-21 2013-12-18 Production of omega-amino fatty acids
CN201310707410.5A CN103881933B (zh) 2012-12-21 2013-12-20 ω-氨基脂肪酸的生产
ARP130104951A AR094464A1 (es) 2012-12-21 2013-12-20 PRODUCCIÓN DE ÁCIDOS w-AMINO GRASOS
BR102013033208A BR102013033208A2 (pt) 2012-12-21 2013-12-23 catalisador de célula integral, uso do mesmo, método para a conversão de um ácido graxo e mistura de reação
JP2013265665A JP6332961B2 (ja) 2012-12-21 2013-12-24 ω−アミノ脂肪酸の製造

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP12199024.6A EP2746397A1 (fr) 2012-12-21 2012-12-21 Fabrication d'acides gras oméga-aminés

Publications (1)

Publication Number Publication Date
EP2746397A1 true EP2746397A1 (fr) 2014-06-25

Family

ID=47471594

Family Applications (2)

Application Number Title Priority Date Filing Date
EP12199024.6A Withdrawn EP2746397A1 (fr) 2012-12-21 2012-12-21 Fabrication d'acides gras oméga-aminés
EP13194396.1A Active EP2746399B1 (fr) 2012-12-21 2013-11-26 Fabrication d'acides gras oméga-aminés

Family Applications After (1)

Application Number Title Priority Date Filing Date
EP13194396.1A Active EP2746399B1 (fr) 2012-12-21 2013-11-26 Fabrication d'acides gras oméga-aminés

Country Status (11)

Country Link
US (1) US9719117B2 (fr)
EP (2) EP2746397A1 (fr)
JP (1) JP6332961B2 (fr)
KR (1) KR102252150B1 (fr)
CN (1) CN103881933B (fr)
AR (1) AR094464A1 (fr)
BR (1) BR102013033208A2 (fr)
ES (1) ES2640712T3 (fr)
HU (1) HUE034426T2 (fr)
MX (1) MX349714B (fr)
SG (2) SG10201605082RA (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20160208226A1 (en) * 2013-06-12 2016-07-21 Commonwealth Scientific And Industrial Research Organisation Transaminase Biocatalysts
WO2018007289A1 (fr) * 2016-07-04 2018-01-11 Evonik Degussa Gmbh Gène alkb mutant

Families Citing this family (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102006025821A1 (de) 2006-06-02 2007-12-06 Degussa Gmbh Ein Enzym zur Herstellung von Mehylmalonatsemialdehyd oder Malonatsemialdehyd
DE102008002715A1 (de) 2008-06-27 2009-12-31 Evonik Röhm Gmbh 2-Hydroxyisobuttersäure produzierende rekombinante Zelle
DE102010043470A1 (de) 2010-11-05 2012-05-10 Evonik Degussa Gmbh Zusammensetzung aus Polyamiden mit niedriger Konzentration an Carbonsäureamidgruppen und elektrisch leitfähigem Kohlenstoff
DE102010043473A1 (de) 2010-11-05 2012-05-10 Evonik Degussa Gmbh Carbon Nanotubes enthaltende Polyamid 12-Zusammensetzung
UA112980C2 (uk) 2011-02-16 2016-11-25 Евонік Дегусса Гмбх Рідкі катіоніти
CA2842000A1 (fr) 2011-07-20 2013-01-24 Evonik Degussa Gmbh Oxydation et amination d'alcools primaires
DE102011084521A1 (de) 2011-10-14 2013-04-18 Evonik Industries Ag Verwendung einer Mehrschichtfolie mit Polyamid- und Polypropylenschichten für die Herstellung photovoltaischer Module
DE102011084518A1 (de) 2011-10-14 2013-04-18 Evonik Industries Ag Verwendung einer Mehrschichtfolie mit Polyamid- und Polyesterschichten fürdie Herstellung photovoltaischer Module
EP2602328A1 (fr) 2011-12-05 2013-06-12 Evonik Industries AG Procédé d'oxydation d'alcanes en utilisant d'une alcane 1-mono-oxygénase AlkB
EP2607490A1 (fr) 2011-12-22 2013-06-26 Evonik Industries AG Procédé de séparation améliorée d'une solution organique hydrophobe et d'un milieu de culture aqueux
EP2607479A1 (fr) 2011-12-22 2013-06-26 Evonik Industries AG Production bio-technologique d'alcools et dérivés associés
EP2631298A1 (fr) 2012-02-22 2013-08-28 Evonik Industries AG Procédé biotechnologique et procédé de production de butanol et d'acide butyrique
EP2639308A1 (fr) 2012-03-12 2013-09-18 Evonik Industries AG Omega-oxydation et -amination enzymatique d'acides gras
DE102012204181A1 (de) 2012-03-16 2013-09-19 Evonik Degussa Gmbh Elektrisch leitfähigen Kohlenstoff enthaltende Polyamidzusammensetzung
WO2013139861A1 (fr) 2012-03-20 2013-09-26 Luc Montagnier Procédés et compositions pharmaceutiques pour le traitement de troubles du syndrome de l'autisme
EP2647696A1 (fr) 2012-04-02 2013-10-09 Evonik Degussa GmbH Procédé de fabrication aérobie d'alanine ou d'une liaison établie sous consommation d'alanine
DE102012207921A1 (de) 2012-05-11 2013-11-14 Evonik Industries Ag Mehrstufiges Syntheseverfahren mit Synthesegas
EP2700448A1 (fr) 2012-08-21 2014-02-26 Evonik Industries AG Acides gras ramifiés comme échangeurs de cations liquides
ES2531144T3 (es) 2012-09-07 2015-03-11 Evonik Industries Ag Composiciones curables a base de resinas epoxídicas sin alcohol bencílico
EP2730655A1 (fr) 2012-11-12 2014-05-14 Evonik Industries AG Procédé de conversion d'un ester d'acide carboxylique en utilisant des cellules déficientes en BioH
EP2746400A1 (fr) * 2012-12-21 2014-06-25 Evonik Industries AG Fabrication d'amines et de diamines à partir d'acide carbonique ou d'acide de dicarbone ou un mono-ester composé de ceux-ci
EP2746397A1 (fr) 2012-12-21 2014-06-25 Evonik Industries AG Fabrication d'acides gras oméga-aminés
EP2759598A1 (fr) 2013-01-24 2014-07-30 Evonik Industries AG Procédé de fabrication d'alpha, oméga-alcane-diol
EP2944697A1 (fr) 2014-05-13 2015-11-18 Evonik Degussa GmbH Procédé de production de nylon
EP2949214A1 (fr) 2014-05-26 2015-12-02 Evonik Degussa GmbH Procédés de production de rhamnolipides
FR3041634B1 (fr) * 2015-09-30 2017-10-20 Arkema France Composition a base d'amino acide ou ester de qualite polymere et procedes d'obtention
KR101903553B1 (ko) * 2015-10-27 2018-10-04 한국생명공학연구원 중쇄 아미노카르복시산의 생산 방법
WO2017102952A1 (fr) 2015-12-17 2017-06-22 Evonik Degussa Gmbh Cellule acétogène génétiquement modifiée
CN107201356A (zh) * 2016-03-17 2017-09-26 中国科学院青岛生物能源与过程研究所 支撑p450脂肪酸脱羧酶活性的还原伴侣蛋白组合及其应用
MY187786A (en) 2016-07-27 2021-10-22 Evonik Operations Gmbh N-acetyl homoserine
CN114181877A (zh) * 2021-12-08 2022-03-15 北京化工大学 一种合成香兰素的基因工程菌及其应用
WO2024096123A1 (fr) * 2022-11-04 2024-05-10 株式会社バイオパレット Micro-organisme génétiquement modifié et son procédé de production

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1119152A2 (fr) 2000-01-19 2001-07-25 Sony Corporation Système de communication de données et dispositif de réception
EP1200766A1 (fr) 1999-07-28 2002-05-02 Coflexip SA Canalisations isolees thermiquement
US20070032428A1 (en) * 2004-09-27 2007-02-08 Amram Mor Novel antimicrobial agents
WO2009077461A1 (fr) * 2007-12-17 2009-06-25 Evonik Degussa Gmbh CELLULES RECOMBINANTES FABRIQUANT DES ACIDES ω-AMINOCARBOXYLIQUES, DES ESTERS D'ACIDES ω-AMINOCARBOXYLIQUES OU LEURS LACTAMES
WO2010135624A2 (fr) 2009-05-22 2010-11-25 Codexis, Inc. Biosynthèse modifiée d'alcools gras

Family Cites Families (84)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10054347A1 (de) 2000-11-02 2002-05-08 Degussa Verfahren zur katalytischen Hydrierung organischer Verbindungen und Trägerkatalysatoren hierfür
DE10142620A1 (de) 2001-08-31 2003-03-20 Degussa Ammoximation von Ketonen und Aufarbeitung durch Pervaporation/Dampfpermeation
DE10142621A1 (de) 2001-08-31 2003-03-20 Degussa Aufarbeitung der Ammoximationsprodukte von Ketonen durch Flüssig-Flüssig-Extraktion in einem ternären Lösemittelsystem
DE10153546A1 (de) 2001-10-30 2003-05-22 Degussa Direktsynthese von Wasserstoffperoxid und deren Integration in Oxidationsprozesse
EP1350788A3 (fr) 2002-03-28 2003-11-12 Degussa AG Procédé pour la préparation d'hexaméthylènediamine à partir de butadiène
EP1350761A1 (fr) 2002-03-28 2003-10-08 Degussa AG Procédé de fabrication de peroxyde d'hydrogène
EP1366812B1 (fr) 2002-05-31 2009-02-18 Evonik Degussa GmbH Catalyseur supporté à base de ruthenium et procédé d'hydrogénation d'amines aromatiques en présence de tel catalyseur
DE10231119A1 (de) 2002-07-10 2004-02-05 Degussa Ag Verfahren zur Selektivitätserhöhung der Hydrierung von 4,4'-Diaminodiphenylmethan zu 4,4'-Diaminodicyclohexylmethan in Gegenwart eines N-Alkyl-4,4'-Diaminodiphenylmethans
DE10247495A1 (de) 2002-10-11 2004-04-22 Degussa Ag Verfahren zur Epoxidierung cyclischer Alkene
EP1424332A1 (fr) 2002-11-26 2004-06-02 Degussa AG Procédé de purification de l'oxyde de propène brut
US7056714B2 (en) * 2003-03-11 2006-06-06 University Of Iowa Research Foundation, Inc. Carboxylic acid reductase polypeptide, nucleotide sequence encoding same and methods of use
US6878836B2 (en) 2003-06-18 2005-04-12 Degussa Ag Process for the epoxidation of propene
DE10344469A1 (de) 2003-09-25 2005-04-14 Degussa Ag Coammoximierung von Ketonen
DE102005053071A1 (de) 2005-11-04 2007-05-16 Degussa Verfahren zur Herstellung von ultrafeinen Pulvern auf Basis Polymaiden, ultrafeinen Polyamidpulver sowie deren Verwendung
DE102006017760A1 (de) 2006-03-24 2007-09-27 Ufz-Umweltforschungszentrum Leipzig-Halle Gmbh Verfahren zur enzymatischen Herstellung von 2-Hydroxy-2-methylcarbonsäuren
DE102006058190A1 (de) 2006-04-28 2007-10-31 Degussa Gmbh Verfahren zur Herstellung von Amiden aus Ketoximen
DE102006022014A1 (de) 2006-05-10 2007-11-15 Degussa Gmbh Verfahren zur Herstellung von Cyclododecatrien
DE102006025821A1 (de) 2006-06-02 2007-12-06 Degussa Gmbh Ein Enzym zur Herstellung von Mehylmalonatsemialdehyd oder Malonatsemialdehyd
DE102007021199B4 (de) 2006-07-17 2016-02-11 Evonik Degussa Gmbh Zusammensetzungen aus organischem Polymer als Matrix und anorganischen Partikeln als Füllstoff, Verfahren zu deren Herstellung sowie deren Verwendung und damit hergestellte Formkörper
DE102007027006A1 (de) 2007-06-08 2008-12-11 Evonik Degussa Gmbh Mikrobiologische Herstellung von Aldehyden, insbesondere von 3-Hydroxypropionaldehyd
DE102007031689A1 (de) 2007-07-06 2009-01-08 Evonik Goldschmidt Gmbh Enzympräparate
CA2728285A1 (fr) * 2008-03-03 2009-09-11 Joule Unlimited, Inc. Microorganismes de synthese fixant le co2 et produisant des produits carbones d'interet
DE102008002090A1 (de) 2008-05-30 2009-12-03 Evonik Degussa Gmbh Ungesättigte Dicarbonsäuren aus ungesättigten cyclischen Kohlenwasserstoffen und Acrylsäure mittels Metathese, deren Verwendung als Monomere für Polyamide, Polyester, Polyurethane sowie weitere Umsetzung zu DIolen und Diaminen
DE102008002715A1 (de) 2008-06-27 2009-12-31 Evonik Röhm Gmbh 2-Hydroxyisobuttersäure produzierende rekombinante Zelle
DE102008040193A1 (de) 2008-07-04 2010-01-07 Evonik Röhm Gmbh Verfahren zur Herstellung freier Carbonsäuren
DE102008040415A1 (de) 2008-07-15 2010-01-21 Evonik Röhm Gmbh Thermisches Salzspalten von Ammoniumcarboxylaten
ES2701501T3 (es) * 2008-10-28 2019-02-22 Reg Life Sciences Llc Célula microbiana para producir alcoholes grasos
DE102009000662A1 (de) 2009-02-06 2010-08-12 Evonik Degussa Gmbh Verfahren zur Herstellung von Aldehyden und Ketonen aus primären und sekundären Alkoholen
DE102009000661A1 (de) 2009-02-06 2010-08-12 Evonik Degussa Gmbh Verfahren zur Herstellung von 2,6-Dioxabicyclo-(3.3.0)-octan-4,8-dion[1S,5S]
DE102009009580A1 (de) 2009-02-19 2010-08-26 Evonik Degussa Gmbh Verfahren zur Herstellung freier Säuren aus ihren Salzen
DE102009002371A1 (de) 2009-04-15 2010-10-21 Evonik Goldschmidt Gmbh Verfahren zur Herstellung von geruchlosen Polyetheralkoholen mittels DMC-Katalysatoren und deren Verwendung in kosmetischen und/oder dermatologischen Zubereitungen
DE102009002811A1 (de) 2009-05-05 2010-11-11 Evonik Degussa Gmbh Enzymatisches Verfahren zur Herstellung von Aldehyden
US8597923B2 (en) * 2009-05-06 2013-12-03 SyntheZyme, LLC Oxidation of compounds using genetically modified Candida
EP2427559A4 (fr) * 2009-05-06 2013-09-18 Dna Twopointo Inc Biotransformation à l aide de candida génétiquement modifié
US8158391B2 (en) * 2009-05-06 2012-04-17 Dna Twopointo, Inc. Production of an α-carboxyl-ω-hydroxy fatty acid using a genetically modified Candida strain
EP3611254B1 (fr) * 2009-05-07 2023-07-05 Genomatica, Inc. Microorganismes et procédés pour la biosynthèse de l'hexaméthylènediamine
JP2012531903A (ja) * 2009-07-02 2012-12-13 バーデザイン, インコーポレイテッド アジピン酸を調製する生物学的方法
DE102009027611A1 (de) 2009-07-10 2011-01-13 Evonik Degussa Gmbh Formmasse auf Basis eines Terephthalsäure- sowie Trimethylhexamethylendiamin-Einheit enthaltenden Copolyamids
US20110015267A1 (en) * 2009-07-20 2011-01-20 Deanna Jean Nelson Methods for the preparation and use of aqueous solutions of magnesium valproate hydrate and l-carnitine
DE102009046626A1 (de) 2009-11-11 2011-05-12 Evonik Degussa Gmbh Candida tropicalis Zellen und deren Verwendung
DE102009046910A1 (de) 2009-11-20 2011-05-26 Evonik Degussa Gmbh Verfahren zur Aufarbeitung eines Laurinlactam enthaltenen Stoffstroms für die Rückgewinnung aller enthaltene Wertstoffkomponenten durch Kombination von Kristallisation mit nachgeschalteter Destillation
BR122019001300B1 (pt) 2009-12-23 2020-03-03 Evonik Degussa Gmbh Processo para produção de adoçantes
AR084377A1 (es) 2010-04-08 2013-05-15 Ls9 Inc Metodos y composiciones relacionados con enzimas de alcohol graso biosintetico
DE102010015807A1 (de) 2010-04-20 2011-10-20 Evonik Degussa Gmbh Biokatalytisches Oxidationsverfahren mit alkL-Genprodukt
DE102010026196A1 (de) 2010-06-25 2011-12-29 Evonik Degussa Gmbh Synthese von omega-Aminocarbonsäuren und deren Estern aus ungesättigten Fettsäurederivaten
DE102010039833A1 (de) * 2010-08-26 2012-03-01 Symrise Ag Ganzzell-Biotransformation von Fettsäuren zu den um ein Kohlenstoffatom verkürzten Fettaldehyden
DE102011004465A1 (de) 2010-09-10 2012-03-15 Evonik Degussa Gmbh Verfahren zur direkten Aminierung sekundärer Alkohole mit Ammoniak zu primären Aminen
DE102010043473A1 (de) 2010-11-05 2012-05-10 Evonik Degussa Gmbh Carbon Nanotubes enthaltende Polyamid 12-Zusammensetzung
DE102010043470A1 (de) 2010-11-05 2012-05-10 Evonik Degussa Gmbh Zusammensetzung aus Polyamiden mit niedriger Konzentration an Carbonsäureamidgruppen und elektrisch leitfähigem Kohlenstoff
WO2012071439A1 (fr) * 2010-11-22 2012-05-31 The Regents Of The University Of California Cellules hôtes et procédés pour produire des diacides
DE102011075162A1 (de) 2010-12-08 2012-06-14 Evonik Degussa Gmbh Verfahren zur homogen-katalysierte, hochselektiven direkten Aminierung von primären Alkoholen mit Ammoniak zu primären Aminen bei hohem Volumenverhältnis von Flüssig- zu Gasphase und/oder hohen Drücken
EP2661487B1 (fr) 2011-01-05 2017-06-28 Verdezyne, Inc. Procédés biologiques pour préparer de l'acide adipique
US20130035513A1 (en) * 2011-01-26 2013-02-07 Ls9, Inc. Methods and compositions for enhanced production of fatty aldehydes and fatty alcohols
UA112980C2 (uk) 2011-02-16 2016-11-25 Евонік Дегусса Гмбх Рідкі катіоніти
RU2013142804A (ru) 2011-02-21 2015-03-27 Эвоник Дегусса Гмбх Способ прямого аминирования спиртов аммиаком до первичных аминов с помощью каталитической системы на основе ксантфоса
DE102011015150A1 (de) 2011-03-25 2012-09-27 Evonik Degussa Gmbh Syntese von alpha, omega-Dicarbonsäuren und deren Estern aus ungesättigten Fettsäurederivaten
DE102011006362A1 (de) 2011-03-29 2012-10-04 Evonik Goldschmidt Gmbh Isopentylester zur Verwendung in kosmetischen, dermatologischen oder pharmazeutischen Kompositionen
ES2537208T3 (es) 2011-04-12 2015-06-03 Evonik Degussa Gmbh Procedimiento realizable continuamente para la preparación de unos compuestos carbonílicos mediante un catalizador que contiene el radical nitroxilo
US8728798B2 (en) * 2011-05-03 2014-05-20 Verdezyne, Inc. Biological methods for preparing adipic acid
US8343752B2 (en) * 2011-05-03 2013-01-01 Verdezyne, Inc. Biological methods for preparing adipic acid
EP2557176A1 (fr) 2011-06-15 2013-02-13 Evonik Degussa GmbH Amination enzymatique
US9334508B2 (en) * 2011-06-17 2016-05-10 Invista North America S.A.R.L. Methods of producing carboxylic acids
US9650653B2 (en) * 2011-06-30 2017-05-16 Invista North America S.A.R.L. Bioconversion process for producing nylon-7, nylon-7,7 and polyesters
CA2842000A1 (fr) 2011-07-20 2013-01-24 Evonik Degussa Gmbh Oxydation et amination d'alcools primaires
JP2014524245A (ja) 2011-08-05 2014-09-22 エボニック デグサ ゲーエムベーハー 二級アルコールの酸化及びアミン化
DE102011110945A1 (de) 2011-08-15 2013-02-21 Evonik Degussa Gmbh Biotechnologisches Syntheseverfahren von organischen Verbindungen mit alkIL-Genprodukt
DE102011110946A1 (de) 2011-08-15 2016-01-21 Evonik Degussa Gmbh Biotechnologisches Syntheseverfahren von omegafunktionalisierten Carbonsäuren und Carbonsäure-Estern aus einfachen Kohlenstoffquellen
DE102011084518A1 (de) 2011-10-14 2013-04-18 Evonik Industries Ag Verwendung einer Mehrschichtfolie mit Polyamid- und Polyesterschichten fürdie Herstellung photovoltaischer Module
DE102011084521A1 (de) 2011-10-14 2013-04-18 Evonik Industries Ag Verwendung einer Mehrschichtfolie mit Polyamid- und Polypropylenschichten für die Herstellung photovoltaischer Module
EP2602328A1 (fr) 2011-12-05 2013-06-12 Evonik Industries AG Procédé d'oxydation d'alcanes en utilisant d'une alcane 1-mono-oxygénase AlkB
US9102960B2 (en) * 2011-12-16 2015-08-11 Invista North America S.á.r.l. Methods of producing 6-carbon chemicals via CoA-dependent carbon chain elongation associated with carbon storage
EP2607479A1 (fr) 2011-12-22 2013-06-26 Evonik Industries AG Production bio-technologique d'alcools et dérivés associés
EP2607490A1 (fr) 2011-12-22 2013-06-26 Evonik Industries AG Procédé de séparation améliorée d'une solution organique hydrophobe et d'un milieu de culture aqueux
DE102011090092A1 (de) 2011-12-29 2013-07-04 Evonik Degussa Gmbh Verfahren zur Herstellung eines Formteils aus einer Polyamidformmasse mit verbesserter Hydrolysebeständigkeit
EP2620504A1 (fr) 2012-01-25 2013-07-31 Evonik Industries AG Procédé d'oxydation d'alcènes en utilisant la monooxygèase AlkB de Pseudomonas putida GPo1
EP2639308A1 (fr) * 2012-03-12 2013-09-18 Evonik Industries AG Omega-oxydation et -amination enzymatique d'acides gras
DE102012204181A1 (de) 2012-03-16 2013-09-19 Evonik Degussa Gmbh Elektrisch leitfähigen Kohlenstoff enthaltende Polyamidzusammensetzung
EP2647696A1 (fr) * 2012-04-02 2013-10-09 Evonik Degussa GmbH Procédé de fabrication aérobie d'alanine ou d'une liaison établie sous consommation d'alanine
WO2013151393A1 (fr) * 2012-04-06 2013-10-10 이화여자대학교 산학협력단 Procédé pour produire des ω-hydroxy-acides gras à chaîne moyenne, des acides α et ω-dicarboxyliques, et des ω-amino-acides gras à partir d'acides gras à chaîne longue par biotransformation
EP2653538A1 (fr) 2012-04-20 2013-10-23 Evonik Industries AG Alanine-déshydrogénase NADP-dépendante
US9532760B2 (en) 2012-04-24 2017-01-03 Siemens Aktiengesellschaft X-ray device
EP2730655A1 (fr) 2012-11-12 2014-05-14 Evonik Industries AG Procédé de conversion d'un ester d'acide carboxylique en utilisant des cellules déficientes en BioH
EP2746397A1 (fr) 2012-12-21 2014-06-25 Evonik Industries AG Fabrication d'acides gras oméga-aminés
DE102013203470A1 (de) 2013-03-01 2014-09-04 Evonik Industries Ag Verfahren zur Herstellung von Ketonen aus Epoxiden

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1200766A1 (fr) 1999-07-28 2002-05-02 Coflexip SA Canalisations isolees thermiquement
EP1119152A2 (fr) 2000-01-19 2001-07-25 Sony Corporation Système de communication de données et dispositif de réception
US20070032428A1 (en) * 2004-09-27 2007-02-08 Amram Mor Novel antimicrobial agents
WO2009077461A1 (fr) * 2007-12-17 2009-06-25 Evonik Degussa Gmbh CELLULES RECOMBINANTES FABRIQUANT DES ACIDES ω-AMINOCARBOXYLIQUES, DES ESTERS D'ACIDES ω-AMINOCARBOXYLIQUES OU LEURS LACTAMES
WO2010135624A2 (fr) 2009-05-22 2010-11-25 Codexis, Inc. Biosynthèse modifiée d'alcools gras

Non-Patent Citations (14)

* Cited by examiner, † Cited by third party
Title
"DIG Easy Hyb", FIRMA ROCHE DIAGNOSTICS GMBH
"Hybaid Hybridisation Guide", 1996, HYBAID LIMITED
"The DIG System User's Guide for Filter Hybridisation", 1995, BOEHRINGER MANNHEIM
"The DIG System Users Guide for Filter Hybridization", 1993, FIRMA BOEHRINGER MANNHEIM GMBH
ARTHUR LESK: "Introduction to bioinformatics", 2008
C. GRANT; J. M. WOODLEY; F. BAGANZ, ENZYME AND MICROBIAL TECHNOLOGY, vol. 48, 2011, pages 480 - 486
F M AUSUBEL: "Current Protocols in Molecular Biology", 1995, JOHN WILEY & SONS, INC.
HI MARRAKCHI; W E DEWOLF; C QUINN; J WEST; B J POLIZZI; C Y SO ET AL., BIOCHEM. J., vol. 370, 2003, pages 1055 - 1062
J. N. COPP ET AL: "The Phosphopantetheinyl Transferase Superfamily: Phylogenetic Analysis and Functional Implications in Cyanobacteria", APPLIED AND ENVIRONMENTAL MICROBIOLOGY, vol. 72, no. 4, 1 April 2006 (2006-04-01), pages 2298 - 2305, XP055063071, ISSN: 0099-2240, DOI: 10.1128/AEM.72.4.2298-2305.2006 *
K KAMEDA; W D NUNN, J. BIOL. CHEM., vol. 256, 1981, pages 5702 - 5707
LIEBL ET AL., INTERNATIONAL JOURNAL OF SYSTEMATIC BACTERIOLOGY, vol. 41, 1991, pages 255 - 260
SAMBROOK; FRITSCH; MANIATIS: "Molecular Cloning: A Laboratory Manual, 2nd edition", 1989, COLD SPRING HARBOR LABORATORY PRESS
SCHEPS, D.; MALCA, H.; HOFFMANN, B.; NESTL, B. M; HAUER, B., ORG. BIOMOL. CHEM., vol. 9, 2011, pages 6727
X YU; T LIU; F ZHU; C KHOSLA, PNAS, 2011

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20160208226A1 (en) * 2013-06-12 2016-07-21 Commonwealth Scientific And Industrial Research Organisation Transaminase Biocatalysts
WO2018007289A1 (fr) * 2016-07-04 2018-01-11 Evonik Degussa Gmbh Gène alkb mutant
EP3336180A1 (fr) * 2016-07-04 2018-06-20 Evonik Degussa GmbH Gène alkb mutante
US11034938B2 (en) 2016-07-04 2021-06-15 Evonik Operations Gmbh Microorganism expressing mutant AlkB enzyme and use to prepare omega-hydroxy carboxylic acid and/or ester

Also Published As

Publication number Publication date
EP2746399A1 (fr) 2014-06-25
ES2640712T3 (es) 2017-11-06
AR094464A1 (es) 2015-08-05
CN103881933A (zh) 2014-06-25
KR102252150B1 (ko) 2021-05-17
MX349714B (es) 2017-08-09
MX2013014727A (es) 2014-06-23
CN103881933B (zh) 2019-04-09
SG2013092010A (en) 2014-07-30
JP6332961B2 (ja) 2018-05-30
SG10201605082RA (en) 2016-08-30
EP2746399B1 (fr) 2017-07-19
JP2014121325A (ja) 2014-07-03
BR102013033208A2 (pt) 2015-09-22
HUE034426T2 (en) 2018-02-28
US9719117B2 (en) 2017-08-01
KR20140090935A (ko) 2014-07-18
US20140178948A1 (en) 2014-06-26

Similar Documents

Publication Publication Date Title
EP2746397A1 (fr) Fabrication d'acides gras oméga-aminés
EP2730655A1 (fr) Procédé de conversion d'un ester d'acide carboxylique en utilisant des cellules déficientes en BioH
EP2639308A1 (fr) Omega-oxydation et -amination enzymatique d'acides gras
EP2935602B1 (fr) Fabrication d'amines et de diamines à partir d'acide carbonique ou d'acide de dicarbone ou un mono-ester composé de ceux-ci
TWI601819B (zh) 丙胺酸之需氧性製造方法或因消耗丙胺酸而產生之化合物的需氧性製造方法
DE102011110946A1 (de) Biotechnologisches Syntheseverfahren von omegafunktionalisierten Carbonsäuren und Carbonsäure-Estern aus einfachen Kohlenstoffquellen
KR102114695B1 (ko) 액체 양이온 교환체로서의 분지쇄 지방산

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20121221

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

AX Request for extension of the european patent

Extension state: BA ME

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

18D Application deemed to be withdrawn

Effective date: 20150106